CN210786770U - Waste gas treatment device for aluminum smelting furnace - Google Patents
Waste gas treatment device for aluminum smelting furnace Download PDFInfo
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- CN210786770U CN210786770U CN201921764398.0U CN201921764398U CN210786770U CN 210786770 U CN210786770 U CN 210786770U CN 201921764398 U CN201921764398 U CN 201921764398U CN 210786770 U CN210786770 U CN 210786770U
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- 238000003723 Smelting Methods 0.000 title claims abstract description 28
- 239000002912 waste gas Substances 0.000 title claims abstract description 25
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 22
- 239000007789 gas Substances 0.000 claims abstract description 81
- 238000009833 condensation Methods 0.000 claims abstract description 56
- 230000005494 condensation Effects 0.000 claims abstract description 56
- 238000001035 drying Methods 0.000 claims abstract description 54
- 239000000428 dust Substances 0.000 claims abstract description 46
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 30
- 238000007789 sealing Methods 0.000 claims description 22
- 238000001179 sorption measurement Methods 0.000 claims description 20
- 238000003780 insertion Methods 0.000 claims description 15
- 230000037431 insertion Effects 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 11
- 239000002893 slag Substances 0.000 claims description 11
- 239000011148 porous material Substances 0.000 claims description 8
- 239000007921 spray Substances 0.000 claims description 7
- 238000001914 filtration Methods 0.000 claims description 6
- 239000000945 filler Substances 0.000 claims description 5
- 238000006477 desulfuration reaction Methods 0.000 claims description 4
- 230000023556 desulfurization Effects 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims 3
- 239000002245 particle Substances 0.000 abstract description 14
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 abstract description 12
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 abstract description 8
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 16
- 239000000126 substance Substances 0.000 description 9
- 238000010586 diagram Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 238000001471 micro-filtration Methods 0.000 description 5
- 239000013618 particulate matter Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000001728 nano-filtration Methods 0.000 description 4
- 239000000741 silica gel Substances 0.000 description 4
- 229910002027 silica gel Inorganic materials 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 239000000809 air pollutant Substances 0.000 description 2
- 231100001243 air pollutant Toxicity 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000004887 air purification Methods 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
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- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
本实用新型提供一种用于铝材熔炼炉的废气处理装置,包括冷凝室和干燥除尘室,所述冷凝室的顶部设有废气出气口,所述干燥除尘室通过所述废气出气口与所述冷凝室连通,所述冷凝室内的侧壁上盘旋设置有螺旋冷凝管,所述冷凝室的底部设有废气进气口,所述废气进气口的上侧设有若干个挡板,且若干个所述挡板依次交替间隔设置于所述冷凝室内的两侧壁上,所述干燥除尘室内间隔设有若干过滤层。该装置不仅能够通过冷凝装置对废气中的热量进行回收,避免大量热量被直接排出,从而减少能源消耗,提高能源利用率;还能够对废气中的微小粒子如PM2.5进行有效截留,对废气中的二氧化硫和氮氧化物进行吸收,避免其随废气排入大气,污染大气环境。
The utility model provides a waste gas treatment device for an aluminum smelting furnace, which comprises a condensation chamber and a drying and dust removal chamber. The top of the condensation chamber is provided with an exhaust gas outlet, and the drying and dust removal chamber communicates with the exhaust gas outlet through the waste gas outlet. The condensing chamber is in communication, the side wall of the condensing chamber is provided with a spiral condensing pipe, the bottom of the condensing chamber is provided with an exhaust gas inlet, and the upper side of the exhaust gas inlet is provided with a number of baffles, and A plurality of the baffles are alternately arranged on the two side walls of the condensation chamber, and a plurality of filter layers are arranged at intervals in the drying and dust removal chamber. The device can not only recover the heat in the exhaust gas through the condensing device to prevent a large amount of heat from being directly discharged, thereby reducing energy consumption and improving energy utilization; it can also effectively intercept tiny particles in the exhaust gas such as PM2. The sulfur dioxide and nitrogen oxides in the waste gas are absorbed to prevent them from being discharged into the atmosphere with the exhaust gas and polluting the atmospheric environment.
Description
技术领域technical field
本实用新型涉及铝材熔炼加工设备领域,具体涉及一种用于铝材熔炼炉的废气处理装置。The utility model relates to the field of aluminum smelting and processing equipment, in particular to a waste gas treatment device for an aluminum smelting furnace.
背景技术Background technique
铝材熔炼是将原材料按工艺要求加入到熔炼炉内熔化,并通过除气、除渣等精炼手段来得到较高纯度的铝液的过程。由于在熔炼的过程中容易产生废气,废气中不仅含有可燃性有机气体,还含有固体颗粒和粉尘等物质,不及时处理,容易对大气环境造成无法预估的破坏,不利于环境保护。Aluminum smelting is a process in which raw materials are added to the smelting furnace for melting according to the process requirements, and higher purity aluminum liquid is obtained by refining methods such as degassing and slag removal. Due to the easy generation of waste gas during the smelting process, the waste gas contains not only combustible organic gases, but also solid particles and dust and other substances. If not treated in time, it is easy to cause unpredictable damage to the atmospheric environment, which is not conducive to environmental protection.
另外,由于铝合金的熔炼温度常在670~750℃范围内,废气在排出的过程中也会从中带走大量的余热,假若不作处理,将会损失大量的热量,因此,需要对废气中的热量进行回收,避免资源的浪费,且能够有效提高能源利用率。In addition, since the melting temperature of aluminum alloy is often in the range of 670-750 °C, the exhaust gas will also take away a lot of waste heat during the discharge process. If it is not treated, a lot of heat will be lost. The heat is recovered to avoid the waste of resources, and can effectively improve the energy utilization rate.
目前,对于铝材熔炼炉的废气处理方法有多种,例如吸附法、吸收法、催化燃烧法、生物氧化法、热处理方法等。相对于其它的处理方法,采用热处理方法处理后的热水能够回收利用,但是现有的处理设备无法将废气中的微小粒子如PM2.5进行截留,也无法对粒径比较小的固体物质,如胶体物质进行有效截留,而PM2.5是雾霾的主要成分,直接排入大气中,将会直接影响大气质量。At present, there are many kinds of waste gas treatment methods for aluminum smelting furnace, such as adsorption method, absorption method, catalytic combustion method, biological oxidation method, heat treatment method, etc. Compared with other treatment methods, the hot water treated by the heat treatment method can be recycled, but the existing treatment equipment cannot intercept tiny particles such as PM2. If colloidal substances are effectively intercepted, and PM2.5 is the main component of smog, it will directly affect the air quality if it is directly discharged into the atmosphere.
实用新型内容Utility model content
为解决上述问题,本实用新型的目的在于提供一种用于铝材熔炼炉的废气处理装置,该装置不仅能够通过冷凝装置对废气中的热量进行回收,避免大量热量被直接排出,从而减少能源消耗,提高能源利用率;还能够对废气中的微小粒子如PM2.5进行有效截留,解决了现有技术中现有的处理设备无法将废气中的微小粒子如PM2.5进行截留,也无法对粒径比较小的固体物质,如胶体物质进行有效截留的问题。In order to solve the above problems, the purpose of the present utility model is to provide a waste gas treatment device for an aluminum smelting furnace, which can not only recover the heat in the waste gas through the condensing device, avoid a large amount of heat being directly discharged, thereby reducing energy It can also effectively intercept tiny particles such as PM2.5 in the exhaust gas, which solves the problem that the existing treatment equipment in the prior art cannot intercept the tiny particles such as PM2.5 in the exhaust gas, and cannot The problem of effective retention of solid substances with relatively small particle size, such as colloidal substances.
为实现上述目的,本实用新型的技术方案如下。To achieve the above purpose, the technical solutions of the present invention are as follows.
一种用于铝材熔炼炉的废气处理装置,包括冷凝室和干燥除尘室,所述冷凝室的顶部设有废气出气口,所述干燥除尘室通过所述废气出气口与所述冷凝室连通,所述冷凝室内的侧壁上盘旋设置有螺旋冷凝管,所述冷凝室的底部设有废气进气口,所述废气进气口的上侧设有若干个挡板,且若干个所述挡板依次交替间隔设置于所述冷凝室内的两侧壁上,所述干燥除尘室内间隔设有若干过滤层。A waste gas treatment device for an aluminum smelting furnace, comprising a condensation chamber and a drying and dust removal chamber, the top of the condensation chamber is provided with an exhaust gas outlet, and the drying and dust removal chamber communicates with the condensation chamber through the waste gas outlet , the side wall of the condensation chamber is provided with a spiral condensation pipe, the bottom of the condensation chamber is provided with an exhaust gas inlet, the upper side of the exhaust gas inlet is provided with a number of baffles, and a number of the The baffles are alternately arranged on the two side walls of the condensation chamber, and a plurality of filter layers are arranged at intervals in the drying and dust removal chamber.
进一步,所述螺旋冷凝管均通过卡接组件与所述冷凝室的侧壁可拆卸连接,所述螺旋冷凝管的一端设有进液口,另一端设有出液口,所述冷凝室靠近所述干燥除尘室的一侧设有进水管,所述冷凝室靠近所述废气出气口的一侧设有出水管,所述螺旋冷凝管的进液口与所述进水管可拆卸连接,所述螺旋冷凝管的出液口与所述出水管可拆卸连接。Further, the spiral condenser tube is detachably connected to the side wall of the condensation chamber through a snap-fit assembly. One end of the spiral condenser tube is provided with a liquid inlet, and the other end is provided with a liquid outlet. The condensation chamber is close to One side of the drying and dust removal chamber is provided with a water inlet pipe, the side of the condensation chamber close to the exhaust gas outlet is provided with a water outlet pipe, and the liquid inlet of the spiral condenser pipe is detachably connected to the water inlet pipe, so the The liquid outlet of the spiral condenser pipe is detachably connected to the water outlet pipe.
进一步,所述螺旋冷凝管朝向所述冷凝室中心的一侧设有若干个喷水口,每个喷水口上均安装有喷头,每个所述喷头均通过密封圈与所述喷水口可拆卸连接;每个所述喷头上均设有电磁阀。Further, the side of the spiral condenser tube facing the center of the condensation chamber is provided with a number of water jets, each of which is installed with a jet, and each of the jets can be connected to the water jet through a sealing ring. Disassemble the connection; each of the spray heads is provided with a solenoid valve.
进一步,所述冷凝室的底部设有排渣口,所述排渣口上安装有筛网,所述排渣口的下端设有卸料漏斗,所述卸料漏斗上设有卸料控制阀。Further, the bottom of the condensation chamber is provided with a slag discharge port, a screen is installed on the slag discharge port, a discharge funnel is provided at the lower end of the slag discharge port, and a discharge control valve is provided on the discharge funnel.
进一步,所述过滤层包括为微滤板和纳滤板,所述微滤板上的滤孔的孔径大于所述纳滤板上的滤孔的孔径,所述微滤板安装于所述干燥除尘室靠近所述废气出气口的一侧。Further, the filter layer includes a microfiltration plate and a nanofiltration plate, the pore size of the filter holes on the microfiltration plate is larger than the pore size of the filter holes on the nanofiltration plate, and the microfiltration plate is installed on the drying The dust chamber is close to the side of the exhaust gas outlet.
进一步,所述干燥除尘室内的侧壁上依次设有若干用于安装与其对应的过滤层相适配的插接槽,每个所述过滤层均可拆卸的安装于与其对应的插接槽内,每个所述过滤层的顶部均设有提手,每个所述插接槽的顶部均设有用于安装所述过滤层的插接孔,每个所述插接孔上均铰接有密封盖。Further, the side walls of the drying and dust removal chamber are sequentially provided with a plurality of insertion slots for installing the corresponding filter layers, and each of the filter layers can be detachably installed in the corresponding insertion slots. , the top of each filter layer is provided with a handle, the top of each plug slot is provided with a plug hole for installing the filter layer, and each plug hole is hinged with a seal cover.
进一步,每个所述过滤层均包括蜂窝芯板以及用于安装所述蜂窝芯板的安装壳体,所述蜂窝芯板的两侧均安装有压合过滤板,每个所述压合过滤板均与所述蜂窝芯板可拆卸连接。Further, each of the filter layers includes a honeycomb core board and a mounting shell for installing the honeycomb core board, and press-fit filter boards are installed on both sides of the honeycomb core board. The boards are all detachably connected to the honeycomb core board.
进一步,所述干燥除尘室远离所述废气出气口的一端上设有气体连接管,所述干燥除尘室靠近所述气体连接管的一侧设有干燥盒,所述干燥盒的顶部设有进料口,所述进料口上设有进料密封门,所述干燥盒的一侧设有出料口,所述出料口上设有出料密封门,所述进料密封门、所述出料密封门均与所述干燥除尘室的侧壁铰接;所述干燥除尘室靠近所述干燥盒的一侧设有透明观察窗。Further, a gas connection pipe is provided on one end of the drying dust chamber away from the exhaust gas outlet, a drying box is provided on the side of the drying dust chamber close to the gas connection pipe, and an inlet is provided on the top of the drying box. The feeding port is provided with a feeding sealing door, one side of the drying box is provided with a discharging port, and the discharging port is provided with a discharging sealing door, the feeding sealing door, the outlet The material sealing doors are hinged with the side wall of the drying and dust removal chamber; a transparent observation window is provided on the side of the drying and dust removal chamber close to the drying box.
进一步,还包括焚烧炉,所述焚烧炉的一侧设有燃烧器,所述焚烧炉通过燃烧器与所述干燥除尘室连接,所述燃烧器的一侧连接有空气进气管。Further, it also includes an incinerator, a burner is provided on one side of the incinerator, the incinerator is connected to the drying and dust removal chamber through the burner, and an air intake pipe is connected to one side of the burner.
更进一步,焚烧炉远离所述燃烧器的一侧设有吸附塔,所述吸附塔的顶端设有排放口,所述吸附塔靠近所述排放口的一侧设有吸附层,所述吸附层内设有脱硫脱硝填料。Further, the side of the incinerator away from the burner is provided with an adsorption tower, the top of the adsorption tower is provided with a discharge port, the side of the adsorption tower close to the discharge port is provided with an adsorption layer, and the adsorption layer is provided with an adsorption layer. There are desulfurization and denitration fillers inside.
本实用新型的有益效果:The beneficial effects of the present utility model:
与现有技术相比,本实用新型提供一种用于铝材熔炼炉的废气处理装置,该装置不仅能够通过冷凝室内的螺旋冷凝管对废气中的热量进行回收,回收热量后的热水能够重新投入使用,避免大量热量被直接排出,从而减少能源消耗,提高能源利用率。Compared with the prior art, the utility model provides a waste gas treatment device for an aluminum smelting furnace, which can not only recover the heat in the waste gas through the spiral condensation pipe in the condensation chamber, but also can recover the hot water after the heat recovery. Put it back into use to avoid a large amount of heat being directly discharged, thereby reducing energy consumption and improving energy utilization.
还能够对废气中的微小粒子如PM2.5进行有效截留,对废气中的二氧化硫和氮氧化物进行吸收,避免其随废气排入大气,污染大气环境;解决了现有技术中现有的处理设备无法将废气中的微小粒子如PM2.5进行截留,也无法对粒径比较小的固体物质,如胶体物质进行有效截留的问题。It can also effectively intercept tiny particles such as PM2.5 in the exhaust gas, absorb sulfur dioxide and nitrogen oxides in the exhaust gas, and prevent them from being discharged into the atmosphere with the exhaust gas and pollute the atmospheric environment; it solves the existing treatment in the prior art. The equipment cannot intercept tiny particles such as PM2.5 in the exhaust gas, nor can it effectively intercept solid substances with relatively small particle sizes, such as colloidal substances.
本实用新型的废气处理装置,采用热处理方法,提高了空气净化效率,降低了投资运行成本,达到经济高效的处理效果,均具有很好的应用前景。The waste gas treatment device of the utility model adopts the heat treatment method, which improves the air purification efficiency, reduces the investment and operation cost, and achieves an economical and efficient treatment effect, all of which have good application prospects.
附图说明Description of drawings
图1为本实用新型实施例1的结构示意图。FIG. 1 is a schematic structural diagram of
图2为本实用新型实施例1中冷凝室的第一视角的结构示意图。FIG. 2 is a schematic structural diagram of a condensation chamber in
图3为本实用新型实施例1中干燥除尘室的结构示意图。3 is a schematic structural diagram of a drying and dust removal chamber in
图4为本实用新型实施例1中过滤层的结构示意图。4 is a schematic structural diagram of a filter layer in
图5为本实用新型实施例2中冷凝室的第二视角的结构示意图。FIG. 5 is a schematic structural diagram of a condensation chamber from a second perspective in
图6为本实用新型实施例3的结构示意图。FIG. 6 is a schematic structural diagram of
图中:1、冷凝室;11、废气进气口;12、废气出气口;13、螺旋冷凝管;131、喷头;14、挡板;15、卡接组件;16、进水管;17、出水管;18、排渣口;181、筛网;19、卸料漏斗;191、卸料控制阀;2、干燥除尘室;21、过滤层;211、微滤板;212、纳滤板;213、蜂窝芯板;214、安装壳体;215、压合过滤板;22、插接槽;23、插接孔;24、密封盖;25、气体连接管;26、干燥盒;261、进料口;262、进料密封门;263出料口;264、出料密封门;27、透明观察窗;3、焚烧炉;31、焚烧炉;32、空气进气管;4、吸附塔;41、排放口;42、吸附层。In the figure: 1. Condensing chamber; 11. Exhaust gas inlet; 12. Exhaust gas outlet; 13. Spiral condenser pipe; 131. Nozzle; 14. Baffle plate; Water pipe; 18, slag outlet; 181, screen; 19, discharge funnel; 191, discharge control valve; 2, drying and dust removal chamber; 21, filter layer; 211, micro filter plate; 212, nano filter plate; 213 , honeycomb core board; 214, installation shell; 215, press-fit filter plate; 22, insertion slot; 23, insertion hole; 24, sealing cover; 25, gas connection pipe; 26, drying box; 261, feeding port; 262, feed sealing door; 263, discharge port; 264, discharge sealing door; 27, transparent observation window; 3, incinerator; 31, incinerator; 32, air intake pipe; 4, adsorption tower; 41, The discharge port; 42, the adsorption layer.
具体实施方式Detailed ways
为了使本实用新型的目的、技术方案及优点更加清楚明白,以下结合附图及实施例,对本实用新型进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本实用新型,并不用于限定本实用新型。In order to make the purpose, technical solutions and advantages of the present utility model more clearly understood, the present utility model will be further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are only used to explain the present invention, and are not intended to limit the present invention.
基于本实用新型中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本实用新型保护的范围。Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work fall within the protection scope of the present invention.
在本实用新型的描述中,“若干”的含义是至少两个,例如两个,三个等,除非另有明确具体的限定。In the description of the present invention, "a number of" means at least two, such as two, three, etc., unless otherwise expressly and specifically defined.
另外,本实用新型各个实施例之间的技术方案可以相互结合,但是必须是以本领域普通技术人员能够实现为基础,当技术方案的结合出现相互矛盾或无法实现时应当认为这种技术方案的结合不存在,也不在本实用新型要求的保护范围之内。In addition, the technical solutions between the various embodiments of the present invention can be combined with each other, but must be based on the realization by those of ordinary skill in the art. When the combination of technical solutions is contradictory or cannot be realized, it should be considered that such technical solutions The combination does not exist and is not within the protection scope required by the present invention.
实施例1Example 1
参见图1-4所示,本实用新型实施例所提供的一种用于铝材熔炼炉的废气处理装置,能够对铝材熔炼炉中的废气进行有效处理,使排出的提起的各项指标均达到大气污染物排放标准。Referring to Figures 1-4, a waste gas treatment device for an aluminum material smelting furnace provided by the embodiment of the present invention can effectively treat the waste gas in the aluminum material smelting furnace, so that the indicators of the discharged lifted All meet air pollutant emission standards.
该装置包括冷凝室1和干燥除尘室2,冷凝室1的顶部设有废气出气口12,干燥除尘室2通过废气出气口12与冷凝室1连通,使经过冷凝室处理后的气体能够通过废气出气口进入到干燥除尘室内。The device includes a
冷凝室1内的侧壁上盘旋设置有螺旋冷凝管13,冷凝室1的底部设有废气进气口11,螺旋冷凝管13均通过卡接组件15与冷凝室1的侧壁可拆卸连接,螺旋冷凝管13的一端设有进液口,另一端设有出液口,冷凝室1靠近干燥除尘室2的一侧设有进水管16,冷凝室1靠近废气出气口12的一侧设有出水管17,螺旋冷凝管13的进液口与进水管16可拆卸连接,螺旋冷凝管13的出液口与出水管17可拆卸连接。A
在此,螺旋冷凝管的进液口和出液口通过法兰分别与进水管和出水管密封连接,用以提高连接处的紧固密封性。由于熔炼炉内的熔炼温度常在670~750℃范围内,较高的温度会使熔炼炉的废气带有较高的热能,因此,在高温废气由底部的废气进气口进入,再由顶部的废气出气口排出的运行过程中,能够对螺旋冷凝管内的冷水进行加热,使水温升高成热水,热水经由出水管重新进入锅炉,由锅炉继续加热成蒸汽供锅炉使用。在这个过程中,高温废气中的热量得到回收,避免了大量热量被直接排出,从而减少了能源消耗量,提高了能源利用率。Here, the liquid inlet and the liquid outlet of the spiral condensing pipe are sealed and connected with the water inlet pipe and the water outlet pipe respectively through flanges, so as to improve the tightness and tightness of the connection. Since the smelting temperature in the smelting furnace is usually in the range of 670-750 °C, the higher temperature will make the exhaust gas of the smelting furnace have higher thermal energy. During the operation of the exhaust gas outlet, the cold water in the spiral condensing tube can be heated to make the water temperature rise to hot water. The hot water re-enters the boiler through the water outlet pipe, and the boiler continues to heat it into steam for the boiler. In this process, the heat in the high-temperature exhaust gas is recovered, preventing a large amount of heat from being directly discharged, thereby reducing energy consumption and improving energy utilization.
为了进一步延长废气在冷凝室内的停留时间,以提高热量转化率,废气进气口11的上侧设有若干个挡板14,且若干个挡板14依次交替间隔设置于冷凝室1内的两侧壁上。冷凝室1的底部设有排渣口18,排渣口18上安装有筛网181,排渣口的下端设有卸料漏斗19,卸料漏斗19上设有卸料控制阀191。In order to further prolong the residence time of the exhaust gas in the condensing chamber and improve the heat conversion rate, a plurality of
本实施例中,废气进气口的上侧设有3个挡板,从下到上依次间隔设有第一挡板、第二挡板和第三挡板。第一挡板位于废气进气口的上方处,第一挡板的一端与冷凝室的内壁固接,另一端与相对另一侧壁之间间隔有距离;第二挡板固定在第一挡板相对的冷凝室的内壁上,且第二挡板与第一挡板固接的冷凝室内壁之间间隔有距离;第三挡板固定在第一挡板相同的冷凝室内壁上,且第三挡板与第二挡板固接的冷凝室内壁之间间隔有距离。In this embodiment, three baffles are arranged on the upper side of the exhaust gas inlet, and a first baffle, a second baffle and a third baffle are arranged in sequence from bottom to top. The first baffle is located above the exhaust gas inlet, one end of the first baffle is fixed to the inner wall of the condensation chamber, and the other end is spaced apart from the opposite side wall; the second baffle is fixed on the first baffle The plates are opposite to the inner wall of the condensation chamber, and there is a distance between the second baffle plate and the inner wall of the condensation chamber to which the first baffle plate is fixed; the third baffle plate is fixed on the same inner wall of the condensation chamber as the first baffle plate, and the third baffle plate is There is a distance between the three baffles and the inner wall of the condenser to which the second baffle is fixedly connected.
熔炼排出的废气中不仅含有很高的热量,还含有大量未燃尽的颗粒物和粉尘,这些物质排入大气会造成大气环境恶化,影响人体健康。本实施例在冷凝室内设置第一挡板、第二挡板和第三挡板不仅能够延长废气在冷凝室内的停留时间,还能够对颗粒物及粉尘进行多级截留。进入冷凝室内的含尘废气中的颗粒物与粉尘首先与第一挡板发生碰撞,从而改变方向下落,而剩余的含尘废气则绕过第一挡板,从第一挡板与冷凝室内壁件的缝隙继续上升,在遇到第二挡板时,气体中所含的粉尘与第二挡板发生碰撞下落,剩余的含尘废气绕过第二挡板,从第二挡板与冷凝室内壁间的缝隙继续上升,最后与第三挡板碰撞,从而改变方向降落。在经过三级碰撞之后,废气中的颗粒物和粉尘基本得到去除。The exhaust gas discharged from smelting not only contains high heat, but also contains a large amount of unburned particulate matter and dust. The discharge of these substances into the atmosphere will cause the deterioration of the atmospheric environment and affect human health. In this embodiment, setting the first baffle, the second baffle and the third baffle in the condensation chamber can not only prolong the residence time of the exhaust gas in the condensation chamber, but also conduct multi-stage interception of particulate matter and dust. The particulate matter and dust in the dust-laden exhaust gas entering the condensing chamber first collide with the first baffle plate, thereby changing direction and falling, while the remaining dust-laden exhaust gas bypasses the first baffle plate and passes from the first baffle plate and the condensation inner wall parts. The gap continues to rise, and when it encounters the second baffle, the dust contained in the gas collides with the second baffle and falls, and the remaining dust-containing exhaust gas bypasses the second baffle and flows from the second baffle and the inner wall of the condenser. The gap between them continued to rise, and finally collided with the third baffle, thereby changing direction and landing. After the three-stage collision, the particulate matter and dust in the exhaust gas are basically removed.
本实施例中,第一挡板与第二挡板有部分重叠,且重叠部分的长度为第二挡板长度的1/10~1/4范围内。第二挡板与第三挡板有部分重叠,且重叠部分的长度为第二挡板长度的1/10~1/4范围内。这样的设置能够使废气呈S型绕行向上,不仅能够延长废气在冷凝室内的停留时间,而且能够有效截留颗粒物及粉尘。In this embodiment, the first baffle plate and the second baffle plate partially overlap, and the length of the overlapping portion is in the range of 1/10-1/4 of the length of the second baffle plate. The second baffle and the third baffle partially overlap, and the length of the overlapping portion is in the range of 1/10-1/4 of the length of the second baffle. Such an arrangement can make the exhaust gas detour upward in an S-shape, which can not only prolong the residence time of the exhaust gas in the condensation chamber, but also effectively trap particulate matter and dust.
而对于废气中的一些粒径比较小的固体物质如胶体物质和PM2.5,冷凝室内的多层挡板无法对其进行有效截留,因此,在冷凝室的上侧设置有一用于除去微小粒子并对气体进行干燥处理的干燥除尘室。For some solid substances with relatively small particle size in the exhaust gas, such as colloidal substances and PM2.5, the multi-layer baffles in the condensation chamber cannot effectively intercept them. A drying and dust-removing chamber that dries the gas.
干燥除尘室2内间隔设有若干过滤层21,用于对微小粒子的过滤截留。Several filter layers 21 are arranged at intervals in the drying and
其中,过滤层21包括为微滤板211和纳滤板212,微滤板211上的滤孔的孔径大于纳滤板212上的滤孔的孔径,方便对废气中的微小粒子进行多级过滤。微滤板211安装于干燥除尘室2靠近废气出气口12的一侧,纳滤板则安装于微滤板远离废气出气口的一侧。由废气出气口排出的废气依次经过微滤板、纳滤板过滤净化,使气体中的固体颗粒及粉尘都得以过滤净化。Wherein, the
为了方便对过滤层进行更换,干燥除尘室2内的侧壁上依次设有若干用于安装与其对应的过滤层21相适配的插接槽22,每个过滤层21均可拆卸的安装于与其对应的插接槽22内,每个过滤层21的顶部均设有提手,每个插接槽22的顶部均设有用于安装过滤层21的插接孔23,每个插接孔23上均铰接有密封盖24。在对过滤层进行更换时,只需打开密封盖就能够将对应的过滤层插接于相应的插接孔内,且沿插接槽插入,提高了更换的效率。In order to facilitate the replacement of the filter layer, a plurality of
每个过滤层21均包括蜂窝芯板213以及用于安装蜂窝芯板213的安装壳体214,蜂窝芯板213的两侧均安装有压合过滤板215,每个压合过滤板215均与蜂窝芯板213可拆卸连接。本实施例中,安装壳体的形状为中空的环形壳体,方便将蜂窝芯板安装于中空部位。Each
干燥除尘室2远离废气出气口12的一端上设有气体连接管25,干燥除尘室2靠近气体连接管25的一侧设有干燥盒26,干燥盒26的顶部设有进料口261,进料口261上设有进料密封门262,干燥盒26的一侧设有出料口263,出料口263上设有出料密封门264,进料密封门262、出料密封门264均与干燥除尘室2的侧壁铰接;干燥除尘室2靠近干燥盒26的一侧设有透明观察窗27。本实施例中,干燥盒内填装有变色硅胶,通过观察窗进可以观察干燥盒内的变色硅胶的颜色,方便及时更换。在更换时,将干燥盒内的变色硅胶由一侧的出料口排出变色硅胶,再关闭出料密封门,从进料口填充入新的变色硅胶,关闭进料密封门,用以提高更换的效率。A
本实施例的干燥除尘室通过过滤层和干燥盒分隔成多个净化室,方便对废气实现多级净化,提高净化程度。The drying and dust removal chamber in this embodiment is divided into a plurality of purification chambers by a filter layer and a drying box, which facilitates multi-stage purification of exhaust gas and improves the degree of purification.
实施例2Example 2
参见图5所示,与上述实施例的不同之处在于,螺旋冷凝管13朝向冷凝室1中心的一侧设有若干个喷水口,每个喷水口上均安装有喷头131,每个喷头131均通过密封圈与喷水口可拆卸连接;每个喷头131上均设有电磁阀。Referring to FIG. 5 , the difference from the above-mentioned embodiment is that the side of the
在冷凝室的外侧设有控制器,控制器与若干个电磁阀电连接,用于控制多个电磁阀的开启。螺旋冷凝管上设有若干个喷头,方便对冷凝室内的固体颗粒进行冲洗,避免过多灰尘堆积在无法清理到的缝隙内。通过控制器控制喷头上的电磁阀的开启,用以提高清洁效率。A controller is provided outside the condensation chamber, and the controller is electrically connected with a plurality of solenoid valves for controlling the opening of the plurality of solenoid valves. There are several nozzles on the spiral condensing pipe, which is convenient for flushing the solid particles in the condensing chamber and avoids excessive dust accumulation in the gaps that cannot be cleaned. The opening of the solenoid valve on the nozzle is controlled by the controller to improve the cleaning efficiency.
实施例3Example 3
参见图6所示,与上述实施例的不同之处在于,还包括焚烧炉3,熔炼炉中产生的废气含有较好含量的可燃性有机气体,因此,需要对这部分有机气体进行燃烧。焚烧炉3的一侧设有燃烧器31,燃烧器内设有低碳氧化物锥形燃烧器,用以加快空气与废气中的可燃性有机气体的混合程度,使其能够充分燃烧。焚烧炉3通过燃烧器31与干燥除尘室2连接,燃烧器31的一侧连接有空气进气管3,空气进气管上设有电磁阀和流量计,用以调节空气的进气量,使可燃性有机废气得以充分燃烧。Referring to FIG. 6 , the difference from the above embodiment is that an
焚烧后的气体中可能含有二氧化硫和氮氧化物,因此,需要对焚烧后的气体进行吸附,以达到排放标准。焚烧炉3远离燃烧器31的一侧设有吸附塔4,吸附塔4的顶端设有排放口41,吸附塔4靠近排放口41的一侧设有吸附层42,吸附层42内设有脱硫脱硝填料。其中,脱硫脱硝填料主要是由氧化镁、氯化镁、磷酸、玻璃纤维以质量比为5:8:0.5:0.5混合制备得到的,在填料中还添加了常用的粘合剂和发泡剂。这些组分能够对废气中的二氧化硫和氮氧化物进行很好的吸附,避免其对大气造成污染。The incinerated gas may contain sulfur dioxide and nitrogen oxides. Therefore, the incinerated gas needs to be adsorbed to meet the emission standards. The side of the
经过上述处理后的废气得到了很好的净化,由吸附塔顶端的排放口排放到大气中,且排出的气体的各项指标均能够达到大气污染物排放标准。The exhaust gas after the above treatment has been well purified, and is discharged into the atmosphere from the discharge port at the top of the adsorption tower, and the indicators of the discharged gas can meet the air pollutant emission standards.
以上仅为本实用新型的较佳实施例而已,并不用以限制本实用新型,凡在本实用新型的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本实用新型的保护范围之内。The above are only preferred embodiments of the present utility model, and are not intended to limit the present utility model. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present utility model shall be included in the present utility model. within the scope of protection.
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CN111888859A (en) * | 2020-09-02 | 2020-11-06 | 黄伟辉 | Energy-concerving and environment-protective type industrial waste gas recovery processing device |
CN114452763A (en) * | 2022-02-14 | 2022-05-10 | 王树青 | Industrial waste gas environmental protection processing apparatus |
CN114484417A (en) * | 2021-12-28 | 2022-05-13 | 湖南田野现代智能装备有限公司 | Biomass combustion furnace |
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Cited By (3)
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CN111888859A (en) * | 2020-09-02 | 2020-11-06 | 黄伟辉 | Energy-concerving and environment-protective type industrial waste gas recovery processing device |
CN114484417A (en) * | 2021-12-28 | 2022-05-13 | 湖南田野现代智能装备有限公司 | Biomass combustion furnace |
CN114452763A (en) * | 2022-02-14 | 2022-05-10 | 王树青 | Industrial waste gas environmental protection processing apparatus |
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